Title of article
Vapor pressure measurement for binary and ternary systems containing a phosphoric ionic liquid
Author/Authors
Zhao، نويسنده , , Jin and Jiang، نويسنده , , Xiaochuan (Edward) Li، نويسنده , , Chun-Xi and Wang، نويسنده , , Zi-Hao، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2006
Pages
9
From page
190
To page
198
Abstract
Vapor pressure data were measured for nine binary systems containing water, methanol or ethanol with the ionic liquids 1-methyl-3-methylimidazolium dimethylphosphate ([MMIM][DMP]), 1-ethyl-3-methylimidazolium diethylphosphate ([EMIM][DEP]) and 1-butyl-3-methylimidazolium dibutylphosphate ([BMIM][DBP]) and one ternary system ethanol–water–[MMIM][DMP] at varying temperature and ionic liquid mass percent ranging from 10% to 70% by a quasi-static method. The vapor pressure data of the binary systems were correlated by NRTL model with overall average absolute relative deviation (ARD) of 0.89% and a maximum ARD within 2%. Based on the vapor pressure depression of binary systems interpolated at ionic liquid mole fraction 0.05 in the temperature range from 280 to 370 K, it is shown that the effect of ionic liquid on the vapor pressure lowering follows the order [MMIM][DMP] > [EMIM][DEP] > [BMIM][DBP] for water, and [BMIM][DBP] > [EMIM][DEP] > [MMIM][DMP] for methanol and ethanol, suggesting that the “ionic” characteristic of the ionic liquid dominates in water, while the “molecule” characteristic prevails in organic solvent. The binary NRTL parameters were used to predict the vapor pressure of the ternary system ethanol–water–[MMIM][DMP] with an ARD of 2.8% and the maximum relative deviation of −5.43%.
Keywords
Ionic liquid , Prediction , vapor pressure , Measurement , NRTL model
Journal title
Fluid Phase Equilibria
Serial Year
2006
Journal title
Fluid Phase Equilibria
Record number
1986109
Link To Document